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2019 (2)

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Dissertation
Controllability Study and Controller Design for a Methane Bioconversion Process
Authors: --- ---
Year: 2019 Publisher: Leuven KU Leuven. Faculteit Ingenieurswetenschappen

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Abstract

Nowadays, global warming is a major scientific and social topic. One of the major contributors to global warming is the emission of methane. The Intergovernmental Panel on Climate Change estimates that 60% of all methane emissions are caused by human activity. Investments in pipelines or methane conversion plants are often not viable due the high capital costs. Hence, new technologies are needed to stimulate methane conversion for smaller sources. An interesting alternative is biological conversion to valueable chemicals with the aid of methanotrophic bacteria. It has the potential to become economically viable for small amounts of methane due to its low capital and operating costs. A promising candidate for industrial processes is Methylomicrobium buryatense 5GB1. It has a high growth rate, robust growth characteristics and can withstand a wide range of growth conditions. This thesis discusses the development of process control tools for such a methane bioconversion process. The main objective is to develop a controller which allows to regulate the biomass and lactate concentration of a methane bioconversion process using Methylomicrobium buryatense 5GB1. This can be divided into the following sub-objectives: (i) the implementation of a controllability study to examine which set of points can be reached (ii) the design and optimization of an integral feedback controller using the linear quadratic regulation problem and (iii) the design of a model predictive controller. A model of the methane bioconversion process is required in order to design process control tools. This is taken from the thesis ’Modelling and Observability Analysis of a Methane Bioconversion Process’ by Koen Michiels. The model is adapted accordingly and then linearized. A controllability study is performed for the linearized model, which concludes that the model is controllable. Next, an integral feedback controller is designed and optimized for the linear model and then applied to the non-linear model. The controller achieves reference tracking for a large range of setpoints and is able to deal with disturbances and measurement noise. Sensitivity analyses are performed to examine to influence of model uncertainties and a linear Kalman filter is implemented as well. Finally, a model predictive controller is designed for the linear model and then applied to the non-linear model. This controller achieves reference tracking faster than the integral feedback controller.

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Dissertation
Monitoring the aerobic cultivation of Escherichia coli using an extended Kalman filter
Authors: --- ---
Year: 2019 Publisher: Leuven KU Leuven. Faculteit Ingenieurswetenschappen

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Monitoring the key components of a biochemical process can be done through online and offline measurements. However, offline measurements are not applicable for online control and available online probes are often unreliable and expensive. The use of a soft sensor can reduce the needed number of online probes by combining sensor data and model predictions. A design of a soft sensor is proposed in this thesis for monitoring a lab-scale aerobic cultivation of E. coli. The extended Kalman filter (EKF) is used for the estimation of optical density (OD), glucose, acetate and dissolved oxygen (DO). The EKF uses a non-linear model for the prediction and online (noisy) measurements for the correction. The employed model captures fermentative and oxidative growth on glucose and the used online measurements are OD and DO. First, the model parameters are identified based on batch and fed-batch data of performed experiments. A confidence interval of the derived parameter estimates is conducted based on the Fisher information matrix. Next, the EKF is fine-tuned and an observability analysis is performed. Two additional augmented EKF's are used and fine-tuned. The first augmented EKF estimates the time-varying oxygen mass transfer coefficient in addition and the second EKF is augmented with the maximum glucose uptake rate to deal with model uncertainties. Lastly, the fine-tuned EKF's are validated. The identified model parameters based on combined batch and fed-batch data showed a low confidence in the glucose saturation constant due to overfeeding of glucose. The estimated acetate inhibition constant was lower compared to values found in literature. Through the condition number of an observability matrix, it is mathematically shown that the EKF cannot observe the real state for certain operating conditions. The EKF is not able to observe high glucose concentrations, as its effect does not show up in the online measurements. Therefore, glucose estimates of the EKF heavily rely on the model prediction. However, glucose estimates deviated from the offline measurements, due to model uncertainties. A high trust in the acetate model estimate was put to limit strong corrections made on the acetate estimate. The fine-tuned EKF was validated on new experimental data. Again, model uncertainties caused a mismatch between glucose estimates and offline measurements, but acetate was very well estimated. The augmented EKF estimated the oxygen mass transfer coefficient well. However, a good performance highly depends on correctly estimated oxygen uptake rates. The augmented EKF estimating the maximum glucose uptake rate showed an improved performance by dealing with model uncertainties.

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